|Publication number||US2872436 A|
|Publication date||Feb 3, 1959|
|Filing date||May 11, 1956|
|Priority date||May 11, 1956|
|Also published as||DE1040239B|
|Publication number||US 2872436 A, US 2872436A, US-A-2872436, US2872436 A, US2872436A|
|Inventors||Billy B Hibbard|
|Original Assignee||Dow Chemical Co|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (4), Referenced by (7), Classifications (11)|
|External Links: USPTO, USPTO Assignment, Espacenet|
United States Patent v 2,872,436 HIGH MOLECULAR WEIGHT VINYLAROMATIC HYDROCARBON MALnrc ANHYDRIDE co- POLYMERS AND PROCESS FOR THEIR PREP- ARATION BillyB. Hibbard, Midland, Mich., assignor to The Dow Chemical Company, Midland, Mich., a corporation of Delaware No Drawing. Application Mayll, 1956 Serial No. 584,165
4 Claims. (Cl. 260-785) This invention relates to a process for preparing a high molecular weight vinylaromatic hydrocarbon-maleic anhydride copolymer, particularly useful as a soil conditioner, and to the products of such process.
Vinylaromatic hydrocarbon-maleic anhydride copolymers of many sorts are well known. They have varied from low to intermediate molecular weight products 'ranging up to a maximum of about 235,000 weight average molecular weight.
In accordance with this invention it has been discovered that an extremely high molecular weight maleic anhydride copolymer of a styrene of the group consisting of styrene and methylstyrenes such as vinyltoluene and vinylxylene or mixtures of any two or more such styrenes, ranging from about 700,000 to 5,500,000 or greater weight average molecular weight, can be prepared by reacting a mixture of approximately equimolar proportions of such a styrene and maleic anhydride, in solution in methylene chloride, within the temperature range of from about 35 to 45 C., in the presence of a catalytic amount of an organic peroxide catalyst.
Solutions of the reactants in methylene chloride varying from about 0.5 to about 33 percent and preferably from about 4 to 6 percent concentration are advantageously used. Below 0.5 percent reactants concentration, the process is uneconomic. Between about 10 and 33 percent reactants concentration, the copolymer which is produced is somewhat more diflicult to handle, in that a thicker slurry is formed. A reactants concentration of from about 4 to 6 percent is most advantageously processed.
The use of methylene chloride as reaction medium is critical. It was most surprising to find that such a high molecular weight styrene-maleic anhydride copolymer could be prepared in the presence of methylene chloride,
since chlorinated hydrocarbons are well known as telomers or chain terminators. Surprisingly, carbon tetrachloride, chloroform, methylene bromide, ethylene dichloride, acetone, toluene, xylene, and the like are not operable in place of methylene chloride to give an equivalent result.
Styrenes of the class consisting of styrene, vinyltolueue and vinylxylene are operable in this invention. The styrene and maleic anhydride can be employed in any do sired proportions, but for convenience are preferably employed in approximately equimolar proportions.
The temperature of the reaction is relatively critical, ranging from about 35 to 45 C. and, preferably, about 40 to 41 C. Higher polymerization temperatures than 45 C. give low molecular weight products, while lower temperatures than 35 C. require an uneconomic expenditure of time.
A catalytic amount of an organic peroxide catalyst such as lauroyl peroxide, benzoyl peroxide, and diacetylperoxide can be used in making these high molecular weight copolymers. Proportions of catalyst ranging from about "0.01 to 6 and preferably from about 0.15 to 1.2 weight percent of monomers are advantageously used. The re- Patented Feb. 3, 19159 action time may vary from several hours to 24 hours or longer, depending in part upon the catalyst concentration.
In practice, the reactants are dissolved in the methylene chloride in the desired proportions. A catalytic amount of an organic peroxide catalyst is added. The mixture is usually agitated and maintained at reaction temperatures of from about 35 to 45 C. As the reaction proceeds, the copolymer precipitates from the solution. Upon completion of the reaction, the slurry can be treated with an alkali, e. g, an aqueous solution of sodium hydroxide, to form a salt of the copolymer. The copolymer is recovered in usual ways, e. g., by filtering or centrifuging.
In accordance with the process of this invention, copolymers are obtained which have a weight average molecular weight range of from about 700,000 to 5,500,000 or greater. A method of determining weight average molecular weights of polymers is described in J. Phys. and C011. Chem. 51, p. 18, 1947. A 0.5% aqueous solution of the sodium salt of a high molecular weight styrene-maleic anhydride copolymer has a pH range of about 7 to 9.5 and a Brookfield viscosity between about centipoises and up to about 4100 centipoises at 25 C. The alkali salts of the copolymers are useful as soil conditioners because of their ability to improve the physical structure of soils.
The following examples represent preferred embodiments of this invention. Parts and percentages therein are by weight.
EXAMPLE 1 A charge of 40.0 parts of styrene and 37.5 parts of maleic anhydride was dissolved in 1422.5 parts of methylene chloride and brought to reflux temperature, 40 to 41 C. Thereafter, 0.0235 part of lauroyl peroxide was added. After refluxing for about 22 hours, the thick slurry which formed was filtered and the product was recovered. The dried copolymer product was obtained in a yield of 86.5 percent as a white powder having a weight average molecular weight of 2,158,000 as measured by light scattering techniques.
EXAMPLE 3 A charge of 40 parts of styrene and 37.5 parts of maleic anhydride was dissolved in 1422 parts of methylene chloride. The solution was brought to reflux tem perature and 0.465 part of lauroyl peroxide was then added. After refluxing for about 22 hours, the thick slurry which formed was filtered and the product rccovered. The dried yield was 90.5 percent copolymer on the basis of starting materials. The weight average molecular weight of this material as determined by light scattering techniques was 5,500,000.
EXAMPLE 4 A charge of 49.4 parts of vinyltoluene and 37.5 parts of maleic anhydride was dissolved in 1425 parts of methylene chloride. The solution was brought to reflux temperature and one part of lauroyl peroxide was then added. After refluxing for about 22 hours, the copolymer product was recovered as a rubbery mass somewhat diificult to dry, but representing an approximately theoretical yield on thebasis of the starting materials. A
small portion was carefully dried and found to have a weight average molecular weight of 3,200,000 as determined by light scattering techniques. 7
EXAMPLE 5 Example 2, and havinga weight average molecular weight of 3,100,000. Combined styrene to vinyltoluene to maleic anhydride in such terpolymer was in the molar ratio of about 0.5 to 0.5 to 1.
EXAMPLE 6 A quantity of 2424 pounds of methylene chloride was pumped into a reactor, 58.8 pounds of maleic anhydride was added slowly thereto and the mixture was stirred for about one hour. Then 62.4 pounds of styrene was added to the reaction mixture and stirred for about fifteen minutes, at which time 0.72 pound of lauroyl peroxide was added. The reaction mixture was then broughtto a reflux temperature of about 40 to 41 C. and held at reflux for 22 hours. An aliquot of the resulting slurry was withdrawn and dried. The weight average molecular weight of the dried copolymer wasdetermined by light scattering techniques to be 1,250,000. The remainder of the copolymer, obtained in 90 percent yield, was neutralized with 50 percent caustic in slurry form, filtered and dried, to give a dried product which, as a 2 percent aqueous solution, had a pH value of 8.25.
The following table illustrates the value of the products of this invention as soil conditioners, in comparison with an untreated soil (control) and with a neutralized styrenemaleic anhydride copolymer, one of the group having the highest molecular weight presently commercially available.
, 4 of 7 to 8 hours each. The results, reported as percolation rate in" cc. per hour, are calculated by dividing the total volume of efiluent by the total number of hours.
Weight of water stable aggregates.The percolation is terminated and the tubes areallowed to drain for 16 hours. The soil column is then slipped out of the tube and a 200 gram (wet weight) longitudinal sample is taken. The sample is placed on a double screen (14 mesh, 32 mesh) and agitated in a tank of water until all of the nonaggregated fines passing 32 mesh are screened out. These water stable aggregates range from 0.5 mm. to 5 mm. in size. The aggregates are weighed after draining five minutes on the screen.
Water retention.--The weight of the soil column is determined immediately after draining 16 hours. As indicated under Percolation rate above, the column was prepared originally with 300 grams of dry soil, and the added weight represents the water held after normal gravity draining.
20 Compaction.The height of the soil column is determined while the soil is still in the percolation tubes. This figure indicates the packing or settling of the soil during the percolation experiments.
What is claimed is:
1. A process for making a high molecular weight copolymer of maleic anhydride and at least one styrene selected from the group consisting of styrene, vinyltoluene, and vinylxylene, which process comprises polymerizing a mixture of approximately equimolecular proportions of the reactants at temperatures between and C. while in admixture with methylene chloride in amount sufiicient to form a solution of the monomers in concentrations between 0.5 and 33 percent and in the presence of a catalytic amount of an organic peroxide until a copolymer having a weight average molecular weight of at least 700,000 is obtained, as determined by the light scattering method.
2. A process as claimed in claim 1 in which the percentage of reactant monomers in solution is from about 4 to 6 percent.
3. A process as claimed in claim 1 in which the reaction temperature ranges from about 40 to 41 C Table I Cone. of Percola Percent Water Column Sample polymer, tion, water-stable retention height, percent cc./hr. aggregates inches N0 soil treatment (Control) none 40 14 32 4. 75 Commercial sample of styrenemaleic anhydride copolymer--." 0. 05 650 60 35 5. 37 Sample of Example 1 0.05 1, 046 61 40 5. 87 Sample of Example 5 0.05 2, 750 64 3O 5. 62
The test procedures used are as follows:
Percolation rate.-The equipment consists of a brass tube, 10 inches long by 1% inches in diameter (inside) with a cast brass base, corrugated on its upper surface and soldered into the bottom (Cenco 28315). On the lower surface of the casting is a nipple for rubber tubing connection. A loose brass disc with small, round perforations fits over the top of the corrugations in the casting,
allowing free passage of air or water through the tube.
A small brass tube is soldered to the outside near the top, with an opening into the soil tube. This construction permits connection of a series of tubes so that a constant water head can be maintained.
A quantity of air-dried Miami silt loam soil is sieved through a IO-mesh screen. A 300 gram portion is used for each tube. The test material is made up to the desired concentration in water and a 25 ml. volume of solution is added to the soil. The samples are then placed in the soil tubes, wetted to saturation and allowed to stand for 72 hours. The tubes are maintained under a constant head and the total volume of water that passes through the soil during a given time interval is measured. This interval is broken into three successive daily runs References Cited in the file of this patent UNITED STATES PATENTS 2,297,351 Gerhart Sept. 29, 1942 2,333,513 Berberich et al Nov. 2, 1943 2,634,256 Sparks et al Apr. 7, 1953 2,675,370 Barrett Apr. 13, 1954 OTHER REFERENCES Debye: J. Phys. and C011. Chem., vol. 5 (1947), pp. 18-31.
Schildknecht: Vinyl and Related Polymers, Wiley & Sons (1952),pp. 65-68.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US2297351 *||Nov 23, 1938||Sep 29, 1942||Pittsburgh Plate Glass Co||Conjoint polymerization of dicarboxylic acids and olefinic compounds|
|US2333513 *||May 3, 1941||Nov 2, 1943||Westinghouse Electric & Mfg Co||Plastic composition|
|US2634256 *||Feb 15, 1949||Apr 7, 1953||Standard Oil Dev Co||Modified olefin-diolefin resin|
|US2675370 *||Jun 28, 1950||Apr 13, 1954||Monsanto Chemicals||Continuous polymerization processes and resulting products|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US3078241 *||Apr 3, 1958||Feb 19, 1963||Dow Chemical Co||Sulfonated vinyl aromatic hydrocarbon-maleic anhydride copolymer composition and useas a soil conditioner|
|US3084070 *||Sep 2, 1958||Apr 2, 1963||Dow Chemical Co||Warp size comprising high molecular weight styrene/maleic anhydride copolymer|
|US3725360 *||Mar 11, 1971||Apr 3, 1973||Dow Chemical Co||Process for polymerizing styrene and maleic anhydride|
|US3972903 *||Jul 26, 1974||Aug 3, 1976||The Dow Chemical Company||Molecular weight control in charge-transfer copolymerization|
|US4594378 *||Mar 25, 1985||Jun 10, 1986||The Lubrizol Corporation||Polymeric compositions, oil compositions containing said polymeric compositions, transmission fluids and hydraulic fluids|
|US4604221 *||Apr 3, 1985||Aug 5, 1986||The Lubrizol Corporation||Nitrogen-containing esters and lubricants containing them|
|US4654403 *||Feb 5, 1986||Mar 31, 1987||The Lubrizol Corporation||Polymeric compositions comprising olefin polymer and nitrogen containing ester of a carboxy interpolymer|
|U.S. Classification||526/227, 526/240, 526/272, 523/131, 526/232.1|
|International Classification||C08F22/04, C08F222/08|
|Cooperative Classification||C08F222/08, C08F22/04|
|European Classification||C08F22/04, C08F222/08|